JP2014062293A - Slag removal device and slag removal method - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a slag removal device for blast furnace equipment that is simple in device configuration and is capable of achieving easy and reliable slag removal and furthermore that can reduce the risks of pipe breakages and the like as much as possible, even in the case where pulverized coal without softening point adjustment is used.SOLUTION: A slag removal device for a blow-pipe, which is installed in a blow-pipe 30 for blowing supplementary fuel of pulverized coal 3 together with hot air 2 from the tuyere of a blast furnace main body producing pig iron from iron ore and in which the slag S of pulverized coal 3 comprises a constituent that fuses by hot air 2 and/or the combustion heat of pulverized coal 3, has an injection nozzle 80 for blowing solid 7 that has a fusion point higher than the temperature near the tuyere and that has a particle size larger than pulverized coal 3 into the pulverized coal 3 and hot air 2 flowing inside the blow-pipe 30, and the injection nozzle 80 supplies solid 7 and at the same time is provided with a solid supply system having an open/close control valve 89.

Description

  The present invention relates to a slag removing device and a slag removing method for a blow pipe applied to a blast furnace facility, and in particular, a slag suitable for a blow pipe for blowing pulverized coal obtained by pulverizing low-grade coal as auxiliary fuel into a furnace together with hot air. The present invention relates to a removing device and a slag removing method.

In the blast furnace facility, raw materials such as iron ore, limestone, and coal are introduced into the main body of the blast furnace, and hot air and pulverized coal (PCI charcoal) as auxiliary fuel are blown from the tuyere at the lower side. It is now possible to produce pig iron from iron ore.
When pulverized coal is blown in such a blast furnace facility, if low grade coal having a low ash melting point of about 1100 to 1300 ° C. such as subbituminous coal or lignite is used as pulverized coal, Oxygen contained in the hot air of about 1200 ° C. used for blowing into the furnace and a part of the pulverized coal exhibit a combustion reaction. As a result, ash having a low melting point (hereinafter referred to as “slag”) Dissolves in the injection lance or tuyere.

The slag thus melted is rapidly cooled by coming into contact with the tuyere that is constantly cooled to protect it from the temperature of the blast furnace. As a result, solid slag adheres to the tuyere, causing a problem of clogging the flow path of the blow pipe.
In order to solve such a problem, when the slag softening point (temperature) in pulverized coal is low, as in the prior art disclosed in Patent Document 1 below, for example, a melting point equal to or higher than the temperature in the blast furnace A softening point adjustment process is performed to prevent slag from adhering to the tuyere.

Patent Document 2 below discloses that slag is removed by driving a solid ball into the tuyere from the furnace outer end of the tuyere.
Furthermore, the following Patent Document 3 discloses that a lance is vibrated by blowing a solid tip having a particle diameter of 1 to 2 mm in order to remove deposits accumulated in a gap formed at the tip of two lances. Has been.

JP-A-5-156330 JP-A-6-192714 JP 2006-63376 A

However, the following problems have been pointed out in the above-described prior art.
The problem with the prior art disclosed in Patent Document 1 is that it is difficult to completely (uniformly) mix pulverized coal and a solid additive (a fossilizer), and as a result, the mixing ratio of the additive is That is, the formation of slag in a portion lower than the predetermined value cannot be prevented. In addition, when an additive is used, a new source of calcium oxide (CaO) such as limestone and serpentine is required, and thus there is a problem that extra costs are generated.

Next, the problem with the prior art disclosed in Patent Document 2 is that not all solid balls collide with the slag. Therefore, if there is a solid ball that does not collide with the slag, this solid ball may collide directly with the inner surface of the blow pipe, and there is a concern that the pipe or the like may be damaged by the collision of the solid ball. In addition, in this patent document 2, the target of the slag damaged by a solid ball is a ventilation tuyere and a heat insulation ring.
Note that the prior art disclosed in Patent Document 3 vibrates the lance and is difficult to apply to blow pipes and tuyere.

From such a background, it is desired that the slag removing device for blow pipes applied to the blast furnace equipment enables slag removal easily and reliably with a simple device configuration without adjusting the softening point. In addition, it is desired that a slag removing device for blow pipes applied to blast furnace equipment reduces the risk of pipe breakage or the like as much as possible, and enables easy and reliable slag removal with the simplest possible device configuration.
The present invention has been made to solve the above-mentioned problems, and the object of the present invention is to remove slag easily and reliably with a simple apparatus configuration even when pulverized coal that does not adjust the softening point is used. Another object of the present invention is to provide a slag removing device and a slag removing method for a blast furnace facility that can be achieved and further reduce the risk of pipe breakage and the like as much as possible.

In order to solve the above problems, the present invention employs the following means.
The slag removing device according to the present invention is provided in a blow pipe that blows pulverized coal as auxiliary fuel together with hot air from the tuyere of a blast furnace body that manufactures pig iron from iron ore, and the hot air and / or the pulverized powder is added to the slag of the pulverized coal. A slag removing device for a blow pipe containing a component that is melted by the combustion heat of charcoal, wherein the pulverized coal flowing in the blow pipe and the hot air have a melting point higher than the temperature near the tuyere and the An injection nozzle that blows a solid having a particle size larger than that of pulverized coal is provided, and the injection nozzle includes a solid supply system that supplies the solid and is provided with an open / close control valve. .

According to such a slag removing apparatus of the present invention, an injection nozzle for blowing a solid having a melting point higher than the temperature near the tuyere and a particle size larger than the pulverized coal is provided in the pulverized coal flowing in the blow pipe and the hot air. The injection nozzle is provided with a solid material supply system that supplies a solid material and is provided with an open / close control valve. Therefore, the solid material blown into the blow pipe from the injection nozzle uses a flow of hot air as a driving force. It progresses without melting and can be removed by applying a mechanical impact to the slag adhering to the vicinity of the tuyere. In this case, the flow of hot air can be used as the propulsion force of the solid matter in the blow pipe.
In addition, as a suitable solid substance, granular coal, slag, a lime grain, a pellet grain, a sintered ore, iron powder etc. can be illustrated, What is necessary is just to mix and use 1 type or multiple types from these.

  Said invention WHEREIN: It is preferable to provide the swirl | flow flow formation part which generate | occur | produces a swirl | vortex flow in the flow of the said hot air in the position which becomes upstream from the injection lance which blows in the said pulverized coal inside the said blow pipe, The blown solid matter receives centrifugal force due to the swirling flow formed in the blow pipe, and intensively collides with the pipe inner surface or tuyere inner surface to which the slag is attached.

In the above invention, an injection nozzle that injects liquid toward a slag adhesion region in the blow pipe is provided, and the injection nozzle includes a liquid supply system that supplies liquid and is provided with an open / close control valve. Preferably, this allows the solid slag adhered by the liquid jet to be rapidly cooled and destroyed and removed by thermal contraction before removing the slag by the solid matter.
The solid injection nozzle and the liquid injection nozzle described above may be provided separately, or an integrated nozzle that can select the injection by switching the flow path by opening / closing the open / close control valve. But you can.

  In the above-described invention, it is preferable that a slag detection means for detecting a slag adhesion state by a differential pressure between the hot air pressure upstream of the injection nozzle and the hot air pressure in the vicinity of the outlet of the blow pipe is preferably provided. Such slag detection means can detect that the adhesion of slag reduces the cross-sectional area of the flow path, and as a result, the differential pressure increases due to an increase in pressure loss.

  In the above invention, when it is determined that the slag adhesion status detected by the slag detection means is equal to or greater than the slag removal threshold, the liquid and / or the solid matter is jetted by opening the open / close control valve and detected by the slag detection means When it is determined that the applied amount of slag is less than the slag removal stop threshold, it is preferable that the opening and closing control valve is closed to stop the injection of the liquid and / or the solid material, and thus the amount of slag attached should be large. Only at times can the liquid from the liquid injection nozzle and the solid matter from the injection nozzle be injected.

  In the above invention, when the slag adhesion state has an alarm output threshold set to a value larger than the slag removal threshold, it can be detected that the slag removal by the liquid ejection nozzle or the ejection nozzle is not performed as scheduled. .

  The slag removal method of the present invention is provided in a blow pipe that blows pulverized coal as auxiliary fuel together with hot air from the tuyere of a blast furnace body that manufactures pig iron from iron ore, and the hot air and / or the pulverized coal into the slag of the pulverized coal. A method for removing slag for a blow pipe containing a component that is melted by the combustion heat of the gas, wherein the pulverized coal flowing in the blow pipe and the hot air have a melting point higher than the temperature near the tuyere and the fine powder A spray nozzle that blows solid matter having a particle size larger than that of charcoal and a spray nozzle that sprays liquid toward the slag adhesion region in the blowpipe, and slag is removed by first spraying the liquid from the spray nozzle first. When the predetermined slag removal cannot be achieved by the first stage slag removal process and the first stage slag removal process, the solidification from the injection nozzle is performed. And it is characterized in that it comprises a and a slag removal step of the second stage of slag removal is carried out alone injects things.

  According to such a slag removal method of the present invention, an injection nozzle that blows solids having a melting point higher than the temperature near the tuyere and a particle size larger than the pulverized coal into the pulverized coal flowing in the blow pipe and hot air, and A first stage slag removal step comprising: a jet nozzle for jetting liquid toward a slag adhesion region in the blow pipe; When the predetermined slag removal cannot be achieved in the slag removal process, it is provided with a second stage slag removal process in which solids are separately injected from the injection nozzle to perform the slag removal. In this case, the first stage of slag removal process by liquid injection with low risk of pipe wear and breakage is preferentially performed, and solid injection is performed only when slag cannot be removed by liquid injection. And performing a second stage of the slag removal step by, thereby enabling more reliable slag removal.

  In the above invention, when a predetermined slag removal cannot be achieved in the second stage slag removal process, a third stage slag removal process is performed in which slag removal is performed by spraying the solid and the liquid together. In this case, the reliability of slag removal is further improved. In this case, a suitable liquid is a flammable liquid such as heavy oil.

  According to the slag removing device and the slag removing method of the present invention described above, since the slag is destroyed and removed by liquid injection or solid matter injection, even if pulverized coal without softening point adjustment is used, a simple device configuration Thus, slag removal can be achieved easily and reliably, and the risk of pipe wear and breakage can be reduced by giving priority to liquid jetting.

  As a result, low-grade coal having an ash melting point as low as about 1100 to 1300 ° C., such as subbituminous coal and lignite, can be used as pulverized coal for auxiliary fuel by reforming it as raw coal. That is, oxygen contained in the hot air of about 1200 ° C. into which the auxiliary fuel is blown reacts with pulverized coal, so that the low melting point slag dissolved by the combustion heat generated by this combustion reaction comes into contact with the low temperature tuyere and rapidly cools. Even if it becomes solid slag and adheres to the tuyere, slag adhered by liquid injection or solid matter injection can be easily destroyed and removed to prevent the flow path of the blow pipe from becoming clogged. .

It is a schematic block diagram which shows one Embodiment of the slag removal apparatus and slag removal method which concern on this invention. It is a schematic block diagram which shows the modification of a swirl flow formation part about the slag removal apparatus and slag removal method shown in FIG. It is a principal part enlarged view explaining the structural example of a slag detection means about the slag removal apparatus and slag removal method shown in FIG. It is a figure which shows the structural example of the blast furnace equipment with which the slag removal apparatus and slag removal method shown in FIG. 1 are applied.

Hereinafter, an embodiment of a slag removing apparatus and a slag removing method according to the present invention will be described with reference to the drawings.
The slag removal apparatus and the slag removal method of this embodiment are used in blast furnace equipment in which pulverized coal, which is low-grade coal, is blown into the blast furnace together with hot air from the tuyere.
For example, in a blast furnace facility as shown in FIG. 4, a raw material 1 such as iron ore, limestone, and coal is supplied from a raw material fixed supply device 10 to a furnace top hopper 21 provided at the top of a blast furnace body 20 via a carry-in conveyor 11. The The lower side wall of the blast furnace main body 20 is provided with a plurality of tuyere 22 arranged at substantially equal pitches in the circumferential direction. Each tuyere 22 is connected to a downstream end of a blow pipe 30 that supplies hot air 2 into the blast furnace body 20. Further, the upstream end of each blow pipe 30 is connected to a hot air supply device 40 which is a supply source of hot air 2 supplied to the inside of the blast furnace body 20.

In the vicinity of the blast furnace body 20, pretreatment (reformation) such as evaporation of moisture in the coal from raw coal (low-grade coal such as subbituminous coal and lignite) is performed, and after this pretreatment, low-grade coal is A pulverized coal production apparatus 50 that is pulverized into pulverized coal is installed.
The reformed pulverized coal (modified coal) 3 produced by the pulverized coal production apparatus 50 is gas-transported to the cyclone separator 60 by a carrier gas 4 such as nitrogen gas. After the gas transported pulverized coal 3 is separated from the transported gas 4 by the cyclone separator 60, it is dropped into the storage tank 70 and stored. The pulverized coal 3 after such reforming is used as blast furnace blown coal (PCI charcoal) of the blast furnace body 20.

  The pulverized coal 3 in the storage tank 70 is supplied into the injection lance (hereinafter referred to as “lance”) 31 of the blow pipe 30 described above. The pulverized coal 3 is combusted by being supplied into the hot air flowing through the blow pipe 30 and forms a flame at the tip of the blow pipe 30 to form a raceway. Thereby, the coal etc. which are contained in the raw material 1 thrown in in the blast furnace main body 20 are burned. As a result, the iron ore contained in the raw material 1 is reduced to become pig iron (molten metal) 5 and taken out from the tap outlet 23.

A suitable property of the pulverized coal 3 that is supplied from the lance 31 to the inside of the blow pipe 30 and becomes the blast furnace blowing coal, that is, a modified pulverized coal (auxiliary fuel) obtained by reforming and pulverizing low-grade coal. The properties are that the oxygen atom content (dry base) is 10 to 18% by weight, and the average pore diameter is 10 to 50 nm (nanometers). The more preferable average pore diameter of the modified pulverized coal is 20 to 50 nm (nanometers).
Such pulverized coal 3 is largely reduced in the main skeleton (C, H, O) although the tar-generating groups of the oxygen-containing functional groups (carboxyl group, aldehyde group, ester group, hydroxyl group, etc.) are greatly reduced. The decomposition (decrease) of the combustion component is greatly suppressed. For this reason, when the hot air 2 is blown into the blast furnace body 20 from the tuyere 22, the main skeleton contains a large amount of oxygen atoms, and the oxygen in the hot air 2 easily diffuses into the charcoal due to the large-diameter pores. In addition, since tar content is very difficult to generate, complete combustion can be achieved with almost no unburned carbon (soot).

  In order to produce (modify) such pulverized coal 3, in the above-described pulverized coal production apparatus 50, low-grade coal such as sub-bituminous coal or lignite as raw coal (dry base oxygen atom content ratio: 18% by weight) A drying step is carried out by heating (110 to 200 ° C. × 0.5 to 1 hour) and drying in a low oxygen atmosphere having an oxygen concentration of 5% by volume or less.

After removing moisture in the drying step described above, the raw coal is heated again in a low oxygen atmosphere (oxygen concentration: 2% by volume or less) (460 to 590 ° C. (preferably 500 to 550 ° C.)) × 0.5 to 1 A dry distillation step is carried out. The raw coal is carbonized by this carbonization process, so that generated water, carbon dioxide and tar are removed as carbonized gas or carbonized oil.
Thereafter, the raw coal that has advanced to the cooling step is cooled (50 ° C. or lower) in a low oxygen atmosphere having an oxygen concentration of 2% by volume or less, and then finely pulverized (particle size: 77 μm or less (80%) Pass)) and is easily manufactured.

In the present embodiment, for example, as shown in FIGS. 1 and 2, the blow pipe 30 is used for the purpose of removing the slag S attached to the inner wall surface of the blow pipe 30, which is a slag adhesion region, the tuyere 22 and the inner wall surface in the vicinity thereof. An injection nozzle 80 is provided for injecting the liquid 6 or the solid material 7 into the inside. For example, one or a plurality of the injection nozzles 80 are provided in the circumferential direction along the inner peripheral surface of the blow pipe 30 as appropriate.
In this case, examples of the suitable liquid 6 ejected from the ejection nozzle 80 include flammable liquids such as water or heavy oil. Moreover, as suitable solid substance 7 injected from the injection nozzle 80, granular coal, slag, a lime grain, a pellet grain, a sintered ore, iron powder, etc. can be illustrated, 1 type or multiple types are mixed from these. Can be used.

The liquid 6 ejected from the ejection nozzle 80 rapidly cools the slag adhering to the vicinity of the blow pipe 30 and the tuyere 22 using the latent heat of vaporization. The slag S that has been rapidly cooled by the injection of the liquid 6 is destroyed by the heat shrinkage and can be easily removed.
On the other hand, the solid material 7 injected from the injection nozzle 80 travels without melting in the blow pipe 30 by using the flow of the hot air 2 as a driving force, and therefore collides with the slag S adhering to the vicinity of the tuyere 22. To do. Therefore, the solid material 7 can collide with the slag S and give a mechanical impact. As a result, the slag S subjected to the collision of the solid material 7 is easily removed because it is destroyed by the impact at the time of the collision.

The injection nozzle 80 is configured so that the outlet opening of the nozzle tip 81 that injects the fluid of the liquid 6 or the solid material 7 is not blocked by the pulverized coal 3 or the slag S. It is desirable that the lance 31 is provided at a position substantially coincident with the tip 31a of the lance 31 or slightly upstream. In this case, the nozzle tip 81 of the injection nozzle 80 preferably has a nozzle shape that injects fluid in the direction of the tuyere 22, particularly liquid in a rod shape, and the injection direction may be variable as necessary. In addition, when making the injection direction of the nozzle tip 81 variable, for example, there is one that swings or turns using the supply pressure of the liquid or solid carrier gas.
Further, the radial position at which the injection nozzle 80 is installed does not become a flow path resistance of the hot air 2 and can be directly irradiated toward the slag S attached to the wall surface of the blow pipe 30. A position close to the wall is desirable.

For example, as shown in FIG. 3, the ejection nozzle 80 is connected to a liquid supply source 83 via a liquid supply pipe 84.
The liquid supply pipe 84 includes, as main components, a supply pump 85 for pressure-feeding the liquid in the liquid supply source 83 to the injection nozzle 80, and a liquid supply (ON / OFF) to the injection nozzle 80 by switching operation of the open / close state. And an open / close control valve 86 for controlling (OFF).

Further, the injection nozzle 80 is connected via a solid supply source 87 and a solid supply pipe 88.
The solid material of the solid material supply source 87 includes a solid material transport gas supply source (not shown) such as nitrogen gas. The solid material supply pipe 88 is provided with an open / close control valve 89 that controls supply (on / off) of solid material to the injection nozzle 80 by switching operation of the open / close state as a main component.

  The opening / closing control of the opening / closing control valves 86 and 89 is performed by the value of the differential pressure ΔP measured by the differential pressure gauge 90. For example, two pressure introduction pipes 90a and 90b are connected to the differential pressure gauge 90 so as to measure the differential pressure ΔP between the hot air mother pipe 32 and the blow pipe downstream position near the tuyere 22 of the blow pipe 30. ing.

  As described above, the ejection nozzle 80 supplies the liquid 6 to be ejected and includes a liquid supply system including the opening / closing control valve 86, and a solid material supply system including the solid material 7 to be ejected and including the opening / closing control valve 89. And a differential pressure gauge (slag detecting means) 90 for detecting a slag state in the slag adhesion region. Therefore, the illustrated injection nozzle 80 selects either the liquid 6 or the solid material 7 from one nozzle tip 81 according to the open / close state of the open / close control valves 86 and 89, or the liquid 6 and the solid material. 7 can be injected simultaneously.

  In the following description, as illustrated, a configuration in which a liquid supply system and a solid material supply system are connected to one injection nozzle 80 will be described, but the configuration is not limited thereto. That is, the liquid supply system and the solid material supply system may be configured to include independent liquid injection nozzles or solid material injection nozzles.

The determination of the amount of slag adhesion is made based on the differential pressure between the hot air pressure upstream of the injection nozzle 80 and the hot air pressure near the outlet of the blow pipe 30.
That is, if slag S adheres to the inner wall surface of the blow pipe 30 or near the tuyere 22, pressure loss occurs due to a reduction in the cross-sectional area of the flow path of the blow pipe 30, so that the blast furnace body is supplied from the hot air mother pipe 32. A pressure drop will occur in the flow of hot air flowing out to 20. Accordingly, the difference between the hot air 2 generated before and after the slag adhesion region by the differential pressure gauge 90 by the pressure introduction pipe 90a connected to the hot air mother pipe 32 and the pressure introduction pipe 90b connected to the blow pipe downstream position of the blow pipe 30. The pressure ΔP is measured, and the adhesion state of the slag S is estimated from the magnitude of the differential pressure ΔP.
The differential pressure ΔP thus measured is used for the opening / closing operation of the opening / closing control valves 86 and 89 described above by comparison with a predetermined threshold value.

By the way, the injection nozzle 80 described above may perform slag removal by spraying the liquid 6 or the solid material 7 alone, or may perform slag removal by simultaneously spraying both the liquid 6 and the solid material 7. May be.
However, as a preferable slag removal method, as the first stage slag removal process, first, the liquid is independently injected from the injection nozzle 80 to perform the slag removal, and the predetermined slag removal is achieved in the first stage slag removal process. In the case where it is not possible, the solid material 7 is jetted independently from the jet nozzle 80 as a second stage slag removing step.
Further, if necessary, a third slag removal is performed by simultaneously injecting the liquid 6 and the solid material 7 from the injection nozzle 80 so that the predetermined slag removal cannot be achieved in the second-stage slag removal process. A step of removing slag may be provided.

That is, the slag removal that injects the liquid 6 has an advantage that the risk of pipe wear or breakage is small as compared with the slag removal that causes the solid 7 to collide.
Accordingly, the first stage of slag removal process by liquid jet is preferentially executed, and only when the slag S cannot be removed by this liquid jet, for example, the slag removal is completed even if the liquid is jetted continuously for a predetermined time. The second stage slag removal step is performed only when it is not possible to confirm that this has been done. As a result, even the slag S that could not be removed by the liquid 6 can be reliably removed using the impact force of the solid material 7.

A more preferable slag removal method cannot achieve predetermined slag removal even in the slag removal process in which the solid substance 7 is independently injected from the injection nozzle 80 as the second stage slag removal process and the solid substance 7 is separately injected in the second stage. In this case, as a third stage slag removal step, the slag removal is performed by simultaneously jetting the liquid 6 and the solid material 7 from the jet nozzle 80. In this third stage slag removing step, it is desirable to use a flammable liquid as the liquid 6.
In the second stage slag removing step, the liquid 6 and the solid material 7 can be simultaneously injected.

  Hereinafter, the opening / closing control of the opening / closing control valves 86 and 89 based on the threshold value of the differential pressure ΔP and the differential pressure ΔP measured by the differential pressure gauge 90 will be specifically described. In the following description, it is assumed that both the liquid 6 and the solid material 7 are ejected at the same time, and the operation of the delivery pump 85 is performed so that the liquid is ejected from the ejection nozzle 80 when the open / close control valve 86 is opened. Is activated.

In the present embodiment, two threshold values, that is, a first threshold value (slag removal threshold value) HL for opening the open / close control valves 86 and 89 in the closed state, and a second threshold value (closing the open / close control valves 86 and 89 in the open state). Slag removal stop threshold) LL.
As for the two threshold values, the same value may be adopted in the slag removing process such as the first stage and the second stage described above, or the first stage slag removing process by liquid jet, for example, is given priority. For example, a larger value may be adopted in the subsequent stage slag removal process than in the first stage slag removal process.

In other words, the first threshold value (slag removal threshold value) HL opens the open / close control valves 86 and 89 when the slag adhesion amount detected by the differential pressure gauge 90 of the slag detection means is greater than or equal to the slag removal threshold value, and opens the liquid 6 And a threshold value for injecting the solid material 7.
The second threshold value (slag removal stop threshold value) LL closes the open / close control valves 86 and 89 when the slag adhesion amount detected by the differential pressure gauge 90 of the slag detection means is smaller than the slag removal stop threshold value. 6 and a threshold value for stopping the injection of the solid material 7.
At the start of operation (at the time of initial setting) where no slag S adheres, the open / close control valves 86 and 89 are set in a closed state, and the differential pressure ΔP detected by the differential pressure gauge 90 is a second threshold value. It is lower than LL and there is almost no differential pressure (ΔP≈0).

When the operation of the blast furnace equipment is continued from the initial setting state described above, the slag S gradually adheres and accumulates on the wall surface at the blow pipe 30 and the tuyere 22, and as a result, the flow path resistance decreases due to the decrease in the cross-sectional area of the flow path. Will gradually increase. Therefore, when the value of the differential pressure ΔP detected by the differential pressure gauge 90 increases and reaches the first threshold value HL, the opening signals of the open / close control valves 86 and 89 are output from the differential pressure gauge 90 that has detected this.
By this open signal, the opening / closing control valves 86 and 89 are opened, and the delivery pump 85 is also started simultaneously. As a result, the liquid 6 stored in the liquid supply source 83 is sprayed from the spray nozzle 80 toward the inside of the blow pipe 30, and at the same time, the solid material 7 stored in the solid material supply source 87 is also It is injected toward the inside of the blow pipe 30 from the injection nozzle 80.

  As a result, when the sprayed liquid 6 hits the attached slag S, it takes away the latent heat of vaporization and rapidly cools. For this reason, this rapid cooling causes the glassy solid and brittle slag S to undergo thermal contraction rapidly, and the slag S that has undergone thermal contraction upon receiving the injection of the liquid 6 is damaged and removed from the wall surface. That is, the slag S that is broken and becomes a relatively small lump is removed into the furnace of the blast furnace body 20 by the hot air 2 or the flow of liquid.

  On the other hand, the injected solid material 7 flows in the direction of the tuyere 22 along the flow of the hot air 2, and when it hits the attached slag S, an impact force is generated so that the brittle slag S is broken with a glassy solid. To break. As a result, the slag S hit by the solid material 7 and received an impact force is broken and removed from the wall surface. That is, the slag S that is broken and becomes a relatively small lump is removed into the furnace of the blast furnace body 20 by the hot air 2 or the flow of liquid.

When the slag S is removed in this way, the flow path resistance decreases with an increase in the cross-sectional area of the flow path, so the differential pressure ΔP detected by the differential pressure gauge 90 also decreases. When the differential pressure ΔP detected by the differential pressure gauge 90 decreases and reaches the second threshold value LL, a closing signal for the opening / closing control valves 86 and 89 is output. The opening / closing control valves 86 and 89 are closed by this closing signal, and the operation of the delivery pump 92 is also stopped at the same time, so that the injection of the liquid 6 and the solid material 7 is stopped.
In order to prevent frequent opening / closing of the opening / closing control valves 86, 89 by providing hysteresis between the first threshold HL described above and the second threshold LL that opens the opening / closing control valves 86, 89, It is set to a slightly large value (HL> LL).

Thus, by providing the injection nozzle 80 for removing the slag S by rapid cooling of the slag S using the latent heat of vaporization of the liquid 6 or pulverization of the slag S using the impact force of the solid 7, Supply equipment such as blast for blowing material is not required. In addition, since liquid such as water and combustible liquid becomes steam or combustion gas after jetting, post-treatment after slag removal is extremely easy if this liquid jetting is prioritized.
In particular, if a flammable liquid such as heavy oil is used as the liquid, the temperature of the hot air can be further increased by burning the flammable liquid.

In the above-described embodiment, two threshold values are set, the first threshold value HL for opening the open / close control valves 86 and 89 in the closed state and the second threshold value LL for closing the open / close control valves 86 and 89 in the open state. However, the third threshold HHL may be set.
The third threshold value HHL is a set value (HHL> HL) that is larger than the first threshold value HL that opens the open / close control valves 86 and 89 in the closed state, and when a differential pressure ΔP exceeding the threshold value HHL is detected. Therefore, it can be determined that there is a problem in removing the slag S. Therefore, when the differential pressure ΔP exceeds the third threshold value HHL, for example, by outputting an alarm to the control room of the blast furnace equipment, etc., it becomes possible to implement necessary measures as soon as possible. It is possible to prevent serious troubles in the blast furnace equipment. That is, the third threshold value HHL is an alarm output threshold value in which the slag adhesion amount is set to a value larger than the first threshold value (slag removal threshold value) HL described above.

  By the way, in the above-described blow pipe 30, the hot air 2 flows between the lance 31 and a position upstream of the lance 31 into which the pulverized coal 3 is blown, that is, between the hot air mother pipe 32 that supplies the hot air 2 and the lance 31. A swirl flow forming part for generating a swirl flow is provided. The swirl flow forming unit may employ a swirl vane 33 as shown in FIG. 1, for example, or may employ a swirl ribbon 34 as shown in FIG. 2 as a modification. The swirl vane 33 is formed by arranging a plurality of vanes having an angle with respect to the flow path cross section in the circumferential direction, and the swirl ribbon 34 is a thin plate formed into a spiral shape.

  Thus, when a swirl flow forming part such as the swirl vane 33 or swirl ribbon 34 swirl flow forming part is provided, the hot air 2 flowing in the blow pipe 30 becomes a swirl flow by passing through the swirl flow forming part. For this reason, the solid material 7 blown out from the injection nozzle 80 is affected by the swirl flow formed in the blow pipe 30, and gathers to the outer peripheral side by centrifugal force. Accordingly, the solid matter 7 collides with the pipe inner surface of the blow pipe 30 to which the slag S adheres or the inner surface of the tuyere 22 intensively, and efficient slag removal becomes possible.

Thus, according to the slag removing apparatus and the slag removing method of the present embodiment described above, the slag S is destroyed and removed by liquid injection or solid injection, so the pulverized coal 3 that does not adjust the softening point is used. Even in this case, slag removal can be achieved easily and reliably with a simple device configuration.
Furthermore, by implementing slag removal giving priority to liquid injection, it is possible to reduce the risk of wear or breakage occurring in the blow pipe 30.
Therefore, the attached slag S can be destroyed and removed without adjusting the softening point of the pulverized coal 3, so that the maintenance period of the blow pipe 30 can be extended to the wear life of the tuyere 22, for example. It becomes.

By the way, the component contained in the slag S of the pulverized coal 3 and melted by the hot air 2 or the combustion heat of the pulverized coal 3, that is, the low melting point slag component is the ash melting point when the hot air 2 of about 1200 ° C. is used. Is approximately 1100 to 1300 ° C. Such a low-melting-point slag component is also included in reformed coal that has been subjected to reforming treatment such as drying or dry distillation using low-grade coal such as subbituminous coal or lignite as the raw coal of pulverized coal 3.
In addition, this invention is not limited to embodiment mentioned above, In the range which does not deviate from the summary, it can change suitably.

1 Raw material 2 Hot air 3 Pulverized coal (modified coal)
4 Carrier gas 5 Pig iron
6 Liquid 7 Solid 10 Raw material metering device 20 Blast furnace body 21 Top hopper 22 Tuyere 30 Blow pipe 31 Injection lance (lance)
32 Hot air mother pipe 33 Swirl vane (swirl flow forming part)
34 Swivel ribbon (swirl flow forming part)
40 Hot Air Supply Device 50 Pulverized Coal Production Device 60 Cyclone Separator 70 Storage Tank 80 Injection Nozzle 81 Nozzle Tip 86, 89 Open / Close Control Valve 90 Differential Pressure Gauge S Slag (Gray)

Claims (8)

A component that is provided in a blow pipe for blowing pulverized coal as auxiliary fuel together with hot air from the tuyere of a blast furnace body that manufactures pig iron from iron ore, and that melts the pulverized coal slag with the hot air and / or the combustion heat of the pulverized coal. A slag removal device for a blowpipe containing,
An injection nozzle that blows a solid material having a melting point higher than the temperature near the tuyere and a particle size larger than that of the pulverized coal in the pulverized coal flowing in the blow pipe and the hot air is provided, A slag removing device comprising a solid material supply system which supplies an object and is provided with an open / close control valve.   The swirl flow forming portion that generates a swirl flow in the flow of the hot air is provided at a position upstream of an injection lance that blows the pulverized coal inside the blow pipe. Slag removal device.   The injection nozzle which injects a liquid toward the slag adhesion area in the blow pipe, The injection nozzle is provided with a liquid supply system provided with an opening / closing control valve while supplying the liquid. The slag removing device according to 1 or 2.   4. The slag detection means for detecting a slag adhesion state based on a differential pressure between a hot air pressure upstream of the injection nozzle and a hot air pressure near the outlet of the blow pipe. 5. The slag removing apparatus according to claim 1.   When it is determined that the slag adhesion state detected by the slag detection means is equal to or greater than the slag removal threshold, the liquid and / or the solid matter is injected by opening the open / close control valve, and the slag adhesion amount detected by the slag detection means is 5. The slag removing device according to claim 4, wherein when it is determined that the amount is less than a slag removal stop threshold, the opening and closing control valve is closed to stop the injection of the liquid and / or the solid matter.   The slag removal device according to claim 5, further comprising an alarm output threshold value in which the slag adhesion state is set to a value larger than the slag removal threshold value. A component that is provided in a blow pipe for blowing pulverized coal as auxiliary fuel together with hot air from the tuyere of a blast furnace body that manufactures pig iron from iron ore, and that melts the pulverized coal slag with the hot air and / or the combustion heat of the pulverized coal. A slag removal method for a blowpipe including:
An injection nozzle that blows solid matter having a melting point higher than the temperature near the tuyere and a particle size larger than the pulverized coal into the pulverized coal flowing in the blowpipe and the hot air, and a slag adhesion region in the blowpipe An injection nozzle for injecting liquid toward
A first stage slag removal step in which slag removal is performed by first jetting the liquid alone from the jet nozzle;
If predetermined slag removal cannot be achieved in the first stage slag removal process, a second stage slag removal process in which slag removal is performed by independently injecting the solid matter from the spray nozzle;
A method for removing slag, comprising: When predetermined slag removal cannot be achieved in the second-stage slag removal process, it comprises a third-stage slag removal process in which slag removal is performed by spraying the solid and the liquid together. The slag removal method according to claim 7.

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